EP3542902B1 - Phases stationnaires d'échange d'anions à base de couche d'hydroxyalkylamine réticulée et de glycidol - Google Patents

Phases stationnaires d'échange d'anions à base de couche d'hydroxyalkylamine réticulée et de glycidol Download PDF

Info

Publication number
EP3542902B1
EP3542902B1 EP19164250.3A EP19164250A EP3542902B1 EP 3542902 B1 EP3542902 B1 EP 3542902B1 EP 19164250 A EP19164250 A EP 19164250A EP 3542902 B1 EP3542902 B1 EP 3542902B1
Authority
EP
European Patent Office
Prior art keywords
ethanolamine
glycidol
groups
polymer layer
anion exchange
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP19164250.3A
Other languages
German (de)
English (en)
Other versions
EP3542902A1 (fr
Inventor
Charanjit Saini
Christopher A. Pohl
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dionex Corp
Original Assignee
Dionex Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US15/928,384 external-priority patent/US10773254B2/en
Priority claimed from US16/101,264 external-priority patent/US10766026B2/en
Application filed by Dionex Corp filed Critical Dionex Corp
Publication of EP3542902A1 publication Critical patent/EP3542902A1/fr
Application granted granted Critical
Publication of EP3542902B1 publication Critical patent/EP3542902B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00—Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/04—Processes using organic exchangers
    • B01J41/07—Processes using organic exchangers in the weakly basic form
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08—Selective adsorption, e.g. chromatography
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08—Selective adsorption, e.g. chromatography
    • B01D15/26—Selective adsorption, e.g. chromatography characterised by the separation mechanism
    • B01D15/36—Selective adsorption, e.g. chromatography characterised by the separation mechanism involving ionic interaction
    • B01D15/361—Ion-exchange
    • B01D15/363—Anion-exchange
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/281—Sorbents specially adapted for preparative, analytical or investigative chromatography
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/3085—Chemical treatments not covered by groups B01J20/3007 - B01J20/3078
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00—Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/04—Processes using organic exchangers
    • B01J41/05—Processes using organic exchangers in the strongly basic form
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00—Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/08—Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/09—Organic material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00—Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/08—Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/12—Macromolecular compounds
    • B01J41/13—Macromolecular compounds obtained otherwise than by reactions only involving unsaturated carbon-to-carbon bonds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00—Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/20—Anion exchangers for chromatographic processes
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02—Column chromatography

Definitions

  • the invention generally relates to anion exchange stationary phases based on a crosslinked hydroxyalkylamine layer and glycidol for applications such as separating samples that include anions, and in particular a combination of haloacetic acids and inorganic anions in a single chromatographic run.
  • Chromatography is a widely used analytical technique for the chemical analysis and separation of molecules. Chromatography involves the separation of one or more analyte species from other matrix components present in a sample.
  • a stationary phase of a chromatography column is typically selected so that there is an interaction with the analyte. Such interactions can be ionic, hydrophilic, hydrophobic, or combinations thereof.
  • the stationary phase can be derivatized with ionic moieties that ideally will bind to ionic analytes and matrix components with varying levels of affinity.
  • a mobile phase is percolated through the stationary phase and competes with the analyte and matrix components for binding to the ionic moieties.
  • the mobile phase or eluent are terms used to describe a liquid solvent or buffer solution that is pumped into a chromatography column inlet.
  • the analyte and matrix components will elute off of the stationary phase as a function of time and then be subsequently detected at a detector.
  • Examples of some typical detectors are a conductivity detector, a UV-VIS spectrophotometer, and a mass spectrometer.
  • chromatography has developed into a powerful analytical tool that is useful for creating a healthier, cleaner, and safer environment where complex sample mixtures can be separated and analyzed for various industries such as water quality, environmental monitoring, food analysis, pharmaceutical, and biotechnology.
  • US 2014/0069870 relates to treatment of anion exchange materials containing hydroxyl containing moieties in the beta position relative to the quaternary center in the hydroxide form with glycidol and this alters the selectivity of the anion exchange material. Furthermore, sequential treatments of first a hydroxide containing solution to put the anion exchange material in the hydroxide form followed by treatment with glycidol in an alternating sequence progressively changes selectivity. This chemistry provides the ability to reverse the elution order of sulfate and carbonate.
  • US 7291395 relates to a method for making an ion exchange coating on a substrate comprising (a) reacting at least a first amine compound comprising amino groups, with at least a first polyfunctional compound, in the presence of a substrate to form a first condensation polymer reaction product, with a first unreacted excess of either at least said first amino group or polyfunctional compound functional moieties, irreversibly attached to the substrate, and (b) reacting at least a second amine compound or at least a second polyfunctional compound with unreacted excess in the first condensation polymer reaction product to form a second condensation polymer reaction product, and repeating the steps to produce the desired coating.
  • a coated ion exchange substrate is so made.
  • haloacetic acids are a group of disinfection byproducts resulting from the reaction between the naturally occurring organic matters and the disinfectants used during water treatment.
  • the presence of haloacetic acids in drinking water has been linked to several adverse effects including bladder, kidney, and colorectal cancer.
  • MCL Maximum Contaminant Level
  • a group of common inorganic anions are routinely monitored in drinking water.
  • the National Primary Drinking Water Standards in the United States specify a Maximum Contaminant Level (MCL) for a number of inorganic anions such as fluoride, nitrite, and nitrate.
  • MCLs are specified to minimize potential health effects arising from the ingestion of these anions in drinking water.
  • High levels of fluoride cause skeletal and dental fluorosis, and nitrite and nitrate can cause methemoglobulinemia, which can be fatal to infants.
  • Other common anions, such as chloride and sulfate are considered secondary contaminants.
  • the National Secondary Drinking Water Standards in the U.S. are guidelines regarding taste, odor, color, and certain aesthetic characteristics. Although these guidelines are not federally enforced, they are recommended to all states as reasonable goals and many states adopt their own regulations governing these contaminants
  • anion exchange stationary phases can have different affinity values to haloacetic acids and common inorganic anions, which makes analysis of both types of chemicals difficult during a single chromatographic run.
  • the retention times of various haloacetic acids and common inorganic anions are sufficiently different, the duration of a single chromatographic run can be unacceptably long.
  • Applicant believes that there is a need for anion exchange stationary phases that require relatively low eluent concentrations and can separate and resolve both haloacetic acids and common inorganic anions in a single relatively fast chromatographic run.
  • a first embodiment of an anion exchange stationary phase includes a negatively charged substrate particle, a base condensation polymer layer, a crosslinked ethanolamine condensation polymer, and a glycidol condensation layer.
  • the base condensation polymer layer is attached to the negatively charged substrate particle.
  • the base condensation polymer layer includes quaternary ammonium groups, ether groups, and hydroxy groups, in which at least a portion of the hydroxy groups is spaced from the quaternary ammonium groups by a first two carbon spacer.
  • the base condensation polymer layer is formed from methylamine and 1,4-butanediol diglycidyl ether.
  • the crosslinked ethanolamine condensation polymer layer is covalently attached to the base condensation polymer layer.
  • the crosslinked ethanolamine condensation polymer layer includes quaternary ammonium groups, ether groups, and hydroxy groups. At least a portion of the ether groups of the crosslinked ethanolamine condensation polymer layer are spaced from the quaternary ammonium groups by a second two carbon spacer. At least a portion of the hydroxy groups of the crosslinked ethanolamine condensation polymer layer are spaced from the quaternary ammonium groups by the first two carbon spacer.
  • the glycidol condensation layer is covalently attached to the crosslinked ethanolamine condensation polymer layer.
  • the glycidol condensation layer includes a plurality of dihydroxy groups, in which each dihydroxy group includes a first hydroxy group and a second hydroxy group.
  • the first hydroxy is spaced from the second hydroxy by the first two carbon spacer, in which at least a portion of the first hydroxy groups are spaced from the quaternary ammonium groups of the crosslinked ethanolamine condensation polymer layer by the first two carbon spacer.
  • the first two carbon spacer includes a chemical formula of and the second two carbon spacer includes a chemical formula of -CH 2 -CH 2 -.
  • a second embodiment is a method of forming an anion exchange stationary phase by reacting 1,4-butanediol diglycidyl ether with methylamine to form a base condensation polymer layer on a negatively charged substrate particle.
  • the base condensation polymer layer is reacted in with a number of reaction cycles to form a crosslinked ethanolamine polymer layer, in which the number of reaction cycles ranges from about three to about ten.
  • Each reaction cycle includes a polyepoxide treatment followed by an ethanolamine treatment.
  • the crosslinked ethanolamine polymer layer is reacted with a first glycidol and then a second glycidol .
  • the anion exchange stationary phase is formed after the glycidol treatments of the crosslinked ethanolamine polymer layer.
  • the method can further include treating the crosslinked ethanolamine polymer layer with a hydroxide solution before each of the first glycidol treatment and the second glycidol treatment.
  • the negatively charged substrate particles are contained in a first column.
  • the reacting of the 1,4-butanediol diglycidyl ether with the methylamine can include flowing a solution of the 1,4-butanediol diglycidyl ether and the methylamine through the first column to form the base condensation polymer layer on the negatively charged substrate particles.
  • the polyepoxide treatment can include flowing a solution of the polyepoxide through the first column and the ethanolamine treatment can include flowing a solution of the ethanolamine through the first column.
  • the first glycidol treatment and the second glycidol treatment can each include flowing a solution of the glycidol through the first column.
  • the method further includes, after the glycidol treatments, removing the packed bed of the anion exchange stationary phase from the first column into a container.
  • the anion exchange stationary phase is treated with a hydroxide solution and then the hydroxide solution is removed.
  • the hydroxide treated anion exchange stationary phase is packed into a second column in which a diameter of the second column is less than the first column.
  • the number of the reaction cycles ranges from about 3 to about 4.
  • the polyepoxide can include a diepoxide compound.
  • the polyepoxide can include an alkyldiol diglycidyl ether.
  • the diepoxide compound can be 1,4-butanediol diglycidyl ether.
  • a third embodiment of an anion exchange stationary phase includes a negatively charged substrate particle, a base condensation polymer layer, a first polyepoxide condensation reaction product, a first ethanolamine condensation reaction product, a second polyepoxide condensation reaction product, a second ethanolamine condensation reaction product, a third polyepoxide condensation reaction product, a third ethanolamine condensation reaction product, a first glycidol condensation reaction product, and a second glycidol condensation reaction product.
  • the anion exchange stationary phase may further include one or more of a fourth, fifth, sixth, seventh, eighth, ninth, and ten polyepoxide condensation reaction products.
  • the anion exchange stationary phase may include one or more of a fourth, fifth, sixth, seventh, eighth, ninth, and ten ethanolamine condensation reaction products.
  • the anion exchange stationary phase may include one or more of a third, fourth, fifth, sixth, seventh, eighth, ninth, and ten glycidol condensation reaction products.
  • the base condensation polymer layer is attached to the negatively charged substrate particle.
  • the base condensation polymer layer includes a reaction product of i) a primary amine and ii) a first polyepoxide compound.
  • the first polyepoxide condensation reaction product can be covalently attached to the base condensation polymer layer.
  • the first polyepoxide condensation reaction product includes a reaction product of i) an amine group of the base condensation polymer layer and ii) a second polyepoxide compound, in which the amine group of the base condensation polymer layer includes a positive charge so that the base condensation polymer layer is ionically coupled to the negatively charged substrate particle.
  • the first ethanolamine condensation reaction product can be covalently attached to the first polyepoxide condensation reaction product.
  • the first ethanolamine condensation reaction product includes a reaction product of i) an epoxide group of the first polyepoxide condensation reaction product, and ii) a first ethanolamine.
  • the second polyepoxide condensation reaction product can be covalently attached to the first ethanolamine condensation reaction product.
  • the second polyepoxide condensation reaction product includes a reaction product of i) an amine group of the first ethanolamine condensation reaction product and ii) a third polyepoxide compound.
  • the second ethanolamine condensation reaction product can be covalently attached to the second polyepoxide condensation reaction product.
  • the second ethanolamine condensation reaction product includes a reaction product of i) an epoxide group of the second polyepoxide condensation reaction product and ii) a second ethanolamine.
  • the third polyepoxide condensation reaction product can be covalently attached to the second ethanolamine condensation reaction product.
  • the third polyepoxide condensation reaction product includes a reaction product of i) an amine group of the second ethanolamine condensation reaction product and ii) a fourth polyepoxide compound.
  • the third ethanolamine condensation reaction product can be covalently attached to the third polyepoxide condensation reaction product.
  • the third ethanolamine condensation reaction product includes a reaction product of i) an epoxide group of the third polyepoxide condensation reaction product and ii) a third ethanolamine.
  • the first glycidol condensation reaction product can be covalently attached to the third ethanolamine condensation product.
  • the first glycidol condensation reaction product includes a reaction product of i) an amine of the third ethanolamine condensation reaction product and ii) a first glycidol.
  • the second glycidol condensation polymer can be covalently attached to the first glycidol condensation product.
  • the second glycidol condensation polymer includes a reaction product of i) a hydroxy group of the first glycidol condensation reaction product, in which a portion of the hydroxy groups of the first glycidol condensation reaction product is spaced from an amine of the third ethanolamine condensation reaction product by a two carbon spacer, and ii) a second glycidol.
  • the second polyepoxide condensation reaction product may further include the reaction product of i) a hydroxy group of the first ethanolamine condensation reaction product, and ii) the third polyepoxide compound.
  • one or more of the second, third, fourth, fifth, sixth, seventh, eighth, ninth, and ten polyepoxide condensation reaction products may further include the reaction product of i) a hydroxy group of one of the ethanolamine condensation reaction products and ii) another polyepoxide compound.
  • the first polyepoxide compound, second polyepoxide compound, third polyepoxide compound, and the fourth polyepoxide compound are each a diepoxide compound.
  • the diepoxide compound may include an alkyldiol diglycidyl ether.
  • the diepoxide compound may include 1,4-butanediol diglycidyl ether.
  • an anion exchange stationary phase for separating haloacetic acids in the presence of inorganic anions.
  • the use includes flowing an eluent through a chromatography column, the chromatography column containing the anion exchange stationary phase, in which the eluent includes a hydroxide.
  • it can further include separating at least one analyte from a sample injected into the chromatography column.
  • the negatively charged substrate particle can include a crosslinked divinylbenzene and ethylvinyl benzene particle, in which at least a surface of the negatively charged substrate particle includes sulfonate groups.
  • the base condensation polymer layer is positively charged and ionically attached to the negatively charged substrate particle.
  • the primary amine can be include alkylamine.
  • the alkylamine can include methylamine.
  • a chromatography column it can contain the anion exchange stationary phases of any one of the first, second, and third embodiments.
  • the chromatography column includes a hollow cylindrical housing, an inlet port, an outlet port, two frits where each one is coupled to the inlet port and the outlet port. Two end fittings can be used to bind the two frits to the respective inlet and outlet ports.
  • alkyl by itself or as part of another substituent, means, unless otherwise stated, a straight or branched chain, or cyclic hydrocarbon radical, or combination thereof, which may be fully saturated, mono- or polyunsaturated and can include di- and multivalent radicals, having the number of carbon atoms designated (i.e., C 1 -C 10 means one to ten carbons).
  • saturated hydrocarbon radicals include, but are not limited to, groups such as methyl, ethyl, n- propyl (e.g., -CH 2 -CH 2 -CH 3 , -CH 2 -CH 2 -CH 2 -), isopropyl, n-butyl, t-butyl, isobutyl, sec- butyl, cyclohexyl, (cyclohexyl)methyl, cyclopropylmethyl, homologs and isomers of, for example, n-pentyl, n-hexyl, n-heptyl, n-octyl, and the like.
  • An unsaturated alkyl group is one having one or more double bonds or triple bonds.
  • unsaturated alkyl groups include, but are not limited to, vinyl, 2-propenyl, crotyl, 2- isopentenyl, 2- (butadienyl), 2,4-pentadienyl, 3-(1,4-pentadienyl), ethynyl, 1 - and 3- propynyl, 3-butynyl, and the higher homologs and isomers.
  • alkyl unless otherwise noted, is also meant to include those derivatives of alkyl defined in more detail below, such as "heteroalkyl”.
  • Alkyl groups that are limited to hydrocarbon groups are termed "homoalkyl".
  • alkyl can also mean "alkylene” or "alkyldiyl” as well as alkylidene in those cases where the alkyl group is a divalent radical.
  • alkylene or "alkyldiyl” by itself or as part of another substituent means a divalent radical derived from an alkyl group, as exemplified, but not limited, by -CH 2 CH 2 CH 2 - (propylene or propane-1,3-diyl), and further includes those groups described below as “heteroalkylene".
  • an alkyl (or alkylene) group will have from 1 to about 30 carbon atoms, preferably from 1 to about 25 carbon atoms, more preferably from 1 to about 20 carbon atoms, even more preferably from 1 to about 15 carbon atoms and most preferably from 1 to about 10 carbon atoms.
  • a “lower alkyl”, “lower alkylene” or “lower alkyldiyl” is a shorter chain alkyl, alkylene or alkyldiyl group, generally having about 10 or fewer carbon atoms, about 8 or fewer carbon atoms, about 6 or fewer carbon atoms or about 4 or fewer carbon atoms.
  • an alkylidene group will have from 1 to about 30 carbon atoms, preferably from 1 to about 25 carbon atoms, more preferably from 1 to about 20 carbon atoms, even more preferably from 1 to about 15 carbon atoms and most preferably from 1 to about 10 carbon atoms.
  • a “lower alkyl” or “lower alkylidene” is a shorter chain alkyl or alkylidene group, generally having about 10 or fewer carbon atoms, about 8 or fewer carbon atoms, about 6 or fewer carbon atoms or about 4 or fewer carbon atoms.
  • alkoxy alkylamino and “alkylthio” (or thioalkoxy) are used in their conventional sense, and refer to those alkyl groups attached to the remainder of the molecule via an oxygen atom, an amino group, or a sulfur atom, respectively.
  • heteroalkyl by itself or in combination with another term, means, unless otherwise stated, a stable straight or branched chain, or cyclic hydrocarbon radical, or combinations thereof, consisting of the stated number of carbon atoms and at least one heteroatom selected from the group consisting of O, N, Si, S and B, and wherein the nitrogen and sulfur atoms may optionally be oxidized and the nitrogen heteroatom may optionally be quaternized.
  • the heteroatom(s) O, N, B, S and Si may be placed at any interior position of the heteroalkyl group or at the position at which the alkyl group is attached to the remainder of the molecule.
  • heteroalkylene by itself or as part of another substituent means a divalent radical derived from heteroalkyl, as exemplified, but not limited by, -CH 2 - CH 2 -S-CH 2 -CH 2 - and -CH 2 -S-CH 2 -CH 2 -NH-CH 2 -.
  • heteroatoms can also occupy either or both of the chain termini (e.g., alkyleneoxy, alkylenedioxy, alkyleneamino, alkylenediamino, and the like).
  • chain termini e.g., alkyleneoxy, alkylenedioxy, alkyleneamino, alkylenediamino, and the like.
  • no orientation of the linking group is implied by the direction in which the formula of the linking group is written.
  • the formula -CO 2 R'- optionally represents both -C(O)OR' and - OC(O)R'.
  • cycloalkyl and “heterocycloalkyl”, by themselves or in combination with other terms, represent, unless otherwise stated, cyclic versions of “alkyl” and “heteroalkyl”, respectively. Additionally, for heterocycloalkyl, a heteroatom can occupy the position at which the heterocycle is attached to the remainder of the molecule. Examples of cycloalkyl include, but are not limited to, cyclopentyl, cyclohexyl, 1 - cyclohexenyl, 3-cyclohexenyl, cycloheptyl, and the like.
  • heterocycloalkyl examples include, but are not limited to, 1-(1,2,5,6-tetrahydropyridyl), 1-piperidinyl, 2-piperidinyl, 3-piperidinyl, 4-morpholinyl, 3-morpholinyl, tetrahydrofuran- 2-yl, tetrahydrofuran-3-yl, tetrahydrothien-2-yl, tetrahydrothien-3-yl, 1 -piperazinyl, 2- piperazinyl, and the like.
  • halo or halogen
  • haloalkyl by themselves or as part of another substituent, mean, unless otherwise stated, a fluorine, chlorine, bromine, or iodine atom.
  • terms such as “haloalkyl,” are meant to include monohaloalkyl and polyhaloalkyl.
  • halo(C 1 -C 4 )alkyl is mean to include, but not be limited to, trifluoromethyl, 2,2,2-trifluoroethyl, 4-chlorobutyl, 3-bromopropyl, and the like.
  • aryl means, unless otherwise stated, a polyunsaturated, aromatic, substituent that can be a single ring or multiple rings (preferably from 1 to 3 rings), which are fused together or linked covalently.
  • heteroaryl refers to aryl groups (or rings) that contain from one to four heteroatoms selected from N, O, S, Si and B, wherein the nitrogen and sulfur atoms are optionally oxidized, and the nitrogen atom(s) are optionally quaternized.
  • a heteroaryl group can be attached to the remainder of the molecule through a heteroatom.
  • Non-limiting examples of aryl and heteroaryl groups include phenyl, 1 - naphthyl, 2-naphthyl, 4-biphenyl, 1 -pyrrolyl, 2-pyrrolyl, 3-pyrrolyl, 3-pyrazolyl, 2-imidazolyl, 4-imidazolyl, pyrazinyl, 2-oxazolyl, 4- oxazolyl, 2-phenyl-4-oxazolyl, 5-oxazolyl, 3-isoxazolyl, 4- isoxazolyl, 5-isoxazolyl, 2- thiazolyl, 4-thiazolyl, 5-thiazolyl, 2-furyl, 3-furyl, 2-thienyl, 3-thienyl, 2-pyridyl, 3- pyridyl, 4-pyridyl, 2-pyrimidyl, 4-pyrimidyl, 5-benzothiazolyl, purinyl, 2-benzimidazolyl, 5-indolyl,
  • aryl when used in combination with other terms (e.g., aryloxy, arylthioxy, arylalkyl) includes both aryl and heteroaryl rings as defined above.
  • arylalkyl is meant to include those radicals in which an aryl group is attached to an alkyl group (e.g., benzyl, phenethyl, pyridylmethyl and the like) including those alkyl groups in which a carbon atom (e.g., a methylene group) has been replaced by, for example, an oxygen atom (e.g., phenoxymethyl, 2- pyridyloxymethyl, 3-(1 - naphthyloxy)propyl, and the like).
  • alkyl group e.g., benzyl, phenethyl, pyridylmethyl and the like
  • an oxygen atom e.g., phenoxymethyl, 2- pyridyloxymethyl, 3-(1 - naph
  • R', R", R′′′ and R ⁇ each preferably independently refer to hydrogen, substituted or unsubstituted heteroalkyl, substituted or unsubstituted aryl, e.g., aryl substituted with 1-3 halogens, substituted or unsubstituted alkyl, alkoxy or thioalkoxy groups, or arylalkyl groups.
  • each of the R groups is independently selected as are each R', R", R′′′ and R ⁇ groups when more than one of these groups is present.
  • R' and R" are attached to the same nitrogen atom, they can be combined with the nitrogen atom to form a 5-, 6-, or 7- membered ring.
  • -NR'R is meant to include, but not be limited to, 1-pyrrolidinyl and 4-morpholinyl.
  • alkyl is meant to include groups including carbon atoms bound to groups other than hydrogen groups, such as haloalkyl (e.g., -CF 3 and -CH 2 CF 3 ) and acyl (e.g., -C(O)CH 3 , -C(O)CF 3 , -C(O)CH 2 OCH 3 , and the like).
  • substituents for the aryl and heteroaryl groups are generically referred to as "aryl group substituents.”
  • sulfonated resin particles can be coated with a reaction product of 1,4-butanediol diglycidyl ether and methylamine to form a base layer on the sulfonated resin particles by electrostatic interaction.
  • a reaction product of 1,4-butanediol diglycidyl ether and methylamine to form a base layer on the sulfonated resin particles by electrostatic interaction.
  • four reaction cycles of 1,4-butanediol diglycidyl ether and ethanolamine were sequentially added to form a crosslinked layer that was hydrophilic and provides divalent anion selectivity.
  • the crosslinked layer may be referred to as a hyperbranched polymer.
  • two glycidol treatments were used in modifying the hyperbranched polymer.
  • glycidol in the hyperbranched architecture provided an added benefit to improve its ability to pack the resin into column tubes.
  • Such glycidol containing hyperbranched architectures are unusually easy to pack with a simple hydroxide packing solution, providing unusually high chromatographic performance compared to similar materials not containing glycidol.
  • Hyperbranched materials not containing glycidol tend to be highly dilatent, shear thickening slurries, which tend to produce fronting peak shape when packed at optimum flow rates. It is believed that glycidol rich phases exhibit less repulsive interactions due to the shielding of the charged groups, which reduces shear thickening behavior and makes them easier to pack into a chromatography column.
  • the resulting stationary phase has many available hydroxy groups to produce crosslinking across and also to aid in maintaining the hydrophilicity of the resin.
  • the hydrophilic highly crosslinked polymer provides good selectivity for haloacetic acid separation along with common anions.
  • Anion exchange stationary phases were synthesized with a crosslinked ethanolamine layer followed by a glycidol treatment that results in a chromatography resin capable of separating haloacetic acid and common inorganic anions in a relatively short single chromatographic run (e.g., less than 20 to 30 minutes). Not only are the chromatographic runs shorter with the anion exchange stationary phases described herein, but lower concentrations of eluent can be employed when performing the single chromatographic run. In general, lower eluent concentrations are desirable for reducing cost and chemical waste.
  • Haloacetic acids are carboxylic acids in which a halogen atom takes the place of a hydrogen atom in acetic acid.
  • haloacetic acids include monochloroacetic acid, dichloroacetic acid, trichloroacetic acid, bromoacetic acid, dibromoacetic acid, tribromoacetic acid, bromochloroacetic acid, bromodichloroacetic acid, and dibromochloroacetic acid.
  • Common inorganic anions include bromate, bromide, chlorate, chloride, chlorite, fluoride, nitrate, nitrite, phosphate, sulfate, and, carbonate, which are often monitored in drinking water (e.g., EPA Method 300.0).
  • anion exchange stationary phases may also be referred to interchangeably as anion exchange resins.
  • the anions chlorite, bromate, and chlorate may also be referred to as oxyhalides.
  • a series of condensation polymer layers and condensation reaction products can be formed on a substrate.
  • a polymer formed in a polymerization reaction with an amine and a polyepoxide may be referred to as a condensation polymer, condensation polymer reaction product, epoxy resin, or epoxy amine resin.
  • a condensation reaction product can be a product from a condensation reaction between a polymer and a reagent (e.g., epoxide or amine based reagent chemical).
  • a polyepoxide includes a compound having two or more epoxide functional groups such as a diepoxide.
  • An example of a polyepoxide may be an alkyldiol diglycidyl ether.
  • polyepoxides include butadiene diepoxide, ethyleneglycol diglycidyl ether, butanediol diglycidyl ether (e.g., 1,4-butanediol diglycidyl ether), diethyleneglycol diglycidyl ether, hexanediol diglycidyl ether, glycerol triglycidyl ether and numerous other compounds containing two or more epoxy groups including epoxy resins commonly used in commercial epoxy formulations.
  • butanediol diglycidyl ether e.g., 1,4-butanediol diglycidyl ether
  • diethyleneglycol diglycidyl ether e.g., 1,4-butanediol diglycidyl ether
  • diethyleneglycol diglycidyl ether e.g., 1,4-butanediol diglycidyl ether
  • Figure 1 illustrates various chemical structures of reagents that can be used in forming condensation polymers and condensation reaction products for anion exchange resins.
  • the reagents illustrated in Figure 1 are 1,4-butanediol diglycidyl ether 102 , methylamine 104 , ethanolamine 106 , and glycidol 108 .
  • Figure 2 illustrates a schematic representation of a base condensation polymer layer 200 attached to a negatively charged substrate particle.
  • the base condensation polymer 200 can be formed by the reaction of a primary amine compound and an alkyldiol diglycidyl ether.
  • the negatively charged substrate particle can be contained as a packed bed in a reaction column.
  • a solution of the polyepoxide and the primary amine can be flowed through the reaction column to form the base condensation polymer layer on the negatively charged substrate particle.
  • the base condensation polymer includes quaternary ammonium groups, ether groups, and hydroxy groups.
  • a primary amine and an alkyldiol diglycidyl ether respectively include a methyl amine 104 and 1,4-butanediol diglycidyl ether 102 (see Figure 1 ).
  • the mole ratio can be a 1:1 mole ratio of primary amine and alkyldiol diglycidyl ether to form the base polymer layer.
  • the base polymer layer is depicted as linear, it is possible for some of the amine groups to be quaternized and form either a branched or crosslinked portions.
  • the base layer 200 can be formed in the presence of a negatively charged polymeric particle where the base layer associates and/or partially binds with the negatively charged polymeric particle, as illustrated in Figure 2 .
  • R may be an alkyl group such as, for example, methyl, ethyl, propyl, butyl, pentyl, or hexyl, but is preferably methyl.
  • n may be value ranging from about 5 to 150.
  • the negatively charged polymeric particle can be any inert polymeric substrate particle that is chemically stable under the intended conditions of use (e.g., pH 0 to 14).
  • the polymeric particle may be based on a divinylbenzene (DVB) crosslinking monomer and a support resin monomer where the support resin monomer may be an ethylvinylbenzene (EVB) monomer, a styrene monomer, and a combination thereof.
  • the mole percent of DVB can be 55% and EVB can be 45%.
  • the support resin particles may have a diameter ranging from about 1 micron to about 20 microns, preferably from about 2 microns to about 10 microns, and more preferably from about 3 microns to about 7 microns.
  • the support resin particles may have a surface area ranging from about 20 m 2 /g to about 800 m 2 /g, preferably from about 20 m 2 /g to about 500 m 2 /g, more preferably from about 20 m 2 /g to about 100 m 2 /g, and yet more preferably be about 20 m 2 /g to about 30 m 2 /g.
  • the support resin particles may have a pore size ranging from about 1000 angstroms to about 2000 angstroms.
  • the negatively charged substrate particle may include one or more super macroporous particles (SMP).
  • SMP can be obtained from commercial sources, including Agilent PLRP-s1000A and Waters Styragel HR4-HR6.
  • the super macroporous particle can have a diameter of 4-6 ⁇ m, a surface area of 20-30 m 2 /g, pore sizes of 1000 ⁇ -2000 ⁇ , and a crosslinking mole ratio of 55% of the divinylbenzene and a mole ratio of 45% of the ethylvinylbenzene.
  • the polymeric particles may be based on other vinylaromatic monomers such as alpha-methylstyrene, chlorostyrene, chloromethylstyrene, vinyltoluene, vinyl naphthalene, and a combination thereof.
  • the polymeric particles may also be based on unsaturated monomers, and copolymers of the above vinylaromatic monomers and unsaturated monomers.
  • such monomers will be copolymerized with a vinylaromatic crosslinking monomer such as divinylbenzene but other vinylaromatic crosslinking monomers such as trivinylbenzene, divinylnaphthalene, and a combination thereof may also be used.
  • the polymeric particles can be sulfonated to create a negative charge at least on the surface of the particle.
  • particles made with 45% DVB and 55% EVB can be sulfonated by treating the particles with glacial acetic acid and concentrated sulfuric acid.
  • base layer 200 can be reacted with at least three reactions cycles of reagents to form a crosslinked ethanolamine polymer layer.
  • Each reaction cycle includes a) a polyepoxide treatment and b) a hydroxyalkylamine treatment.
  • the polyepoxide treatment can include flowing a solution of the polyepoxide through the reaction column and the hydroxyalkylamine treatment can include flowing a solution of the ethanolamine through the reaction column.
  • alkyldiol diglycidyl ether can be reacted with base layer 200 to form a first polyepoxide condensation reaction product (CRP) 300 having pendant epoxide groups 304 , as illustrated in Figure 3 .
  • CRP polyepoxide condensation reaction product
  • the tertiary amines of base layer 200 are converted to quaternary ammonium groups that have a positive charge. It is worthwhile to note that such positive charges are believed to help base layer 200 to ionically bond to the negatively charged particles.
  • at least a portion of the hydroxy groups 202 are spaced from the quaternary ammonium groups by a two carbon spacer.
  • the first polyepoxide CRP 300 can be covalently attached to the base condensation polymer 200 .
  • the first polyepoxide CRP 300 includes a reaction product of i) an amine group of the base condensation polymer 200 , and ii) a second polyepoxide compound, in which the amine group of the base condensation polymer includes a positive charge so that the base condensation polymer 200 is ionically coupled to the negatively charged substrate particle.
  • the pendant epoxide groups 304 can be reacted with a first ethanolamine to form a first ethanolamine CRP 400 , as illustrated in Figure 4 .
  • the first ethanolamine CRP 400 includes a secondary amine 404 and a pendant hydroxy compound 402 , as illustrated in Figure 4 .
  • the first ethanolamine CRP 400 can be covalently attached to the first polyepoxide CRP 300 .
  • the first ethanolamine CRP 400 includes a reaction product of i) an epoxide group 304 of the first polyepoxide CRP 300 , and ii) a first ethanolamine.
  • a second cycle of two steps may be performed to create a hyperbranched structure.
  • the pendant hydroxy group 402 and the secondary amine compound 404 can be reacted with one alkyldiol diglycidyl ethers and two alkyldiol diglycidyl ethers, respectively, to form the second polyepoxide CRP (500b and 500a).
  • the second polyepoxide CRP (500b and 500a ) can be covalently attached to the first ethanolamine CRP 400 .
  • the second polyepoxide CRP (500b and 500a ) includes a reaction product of i) an amine group 404 of the first ethanolamine CRP 400 , and ii) a third polyepoxide compound. Under certain circumstances, the second polyepoxide CRP (500b and 500a ) can further include a reaction product of i) a hydroxy group 402 of the first ethanolamine CRP 400 , and ii) a third polyepoxide compound. As illustrated in Figure 5 , one pendant epoxide branch 500b can be formed from the pendant hydroxy group 402 and two pendant epoxide branches 500a can be formed from the secondary amine group 404 .
  • the secondary amine 404 is converted to a quaternary ammonium group that has a positive charge. It should be noted that the reactivity of pendant hydroxy group 402 may be less than that of the secondary amine group 404 with the epoxy groups. Thus, the proportion of branch 500b may be less than branch 500a.
  • Figure 5 illustrates each diepoxide compound as only reacting with one of the two epoxide groups with first ethanolamine CRP 400 , it is possible for a proportion of diepoxide compounds to crosslink by reacting both of two epoxide groups with the first ethanolamine CRP 400 , or one epoxy group of the diepoxide with the first ethanolamine CRP 400 and the other epoxy group of the diepoxide with a different ethanolamine CRP 400 .
  • the pendant epoxide groups 504 can then be reacted with a second ethanolamine to form a second ethanolamine CRP 600 that has a pendant hydroxy group 602 along with a secondary amine 604 , as illustrated in Figure 6 .
  • the second ethanolamine CRP 600 can be covalently attached to the second polyepoxide CRP ( 500a and 500b ).
  • the second ethanolamine CRP 600 includes a reaction product of i) an epoxide group 504 of the second polyepoxide CRP ( 500a and 500b ), and ii) a second ethanolamine.
  • Figure 6 illustrates each ethanolamine compound as only reacting with one pendant epoxide group, it is possible for a proportion of the ethanolamine compounds to react with two different pendant epoxide groups causing a crosslink.
  • a third reaction cycle of two steps can be performed with the second ethanolamine CRP 600 .
  • the pendant hydroxy group 602 and the secondary amine compound 604 can be reacted with one alkyldiol diglycidyl ethers and two alkyldiol diglycidyl ethers, respectively, to form the third polyepoxide CRP (not shown).
  • the third polyepoxide CRP can be covalently attached to the second ethanolamine CRP 600 .
  • the third polyepoxide CRP includes a reaction product of i) an amine group of the second ethanolamine condensation reaction product, and ii) a fourth polyepoxide compound. It should be noted that the third polyepoxide CRP includes pendant epoxide groups and have a chemical structure analogous to the second polyepoxide CRP ( 500a and 500b of Figure 5 ).
  • the pendant epoxide groups of the third polyepoxide CRP can then be reacted with a third ethanolamine to form a third ethanolamine CRP (not shown).
  • the third ethanolamine CRP can be covalently attached to the third polyepoxide condensation reaction product.
  • the third ethanolamine CRP includes a reaction product of i) an epoxide group of the third polyepoxide condensation reaction product, and ii) a third ethanolamine. It should be noted that the third ethanolamine CRP would have a chemical structure analogous to the second ethanolamine CRP ( 600 of Figure 6 ).
  • a fourth reaction cycle can be performed with the third ethanolamine CRP.
  • the third ethanolamine CRP is reacted with alkyldiol diglycidyl ether and then a fourth ethanolamine to form a fourth polyepoxide CRP (not shown) and a fourth ethanolamine CRP (not shown).
  • the fourth polyepoxide CRP and the ethanolamine CRP would have a chemical structure analogous to the second polyepoxide CRP ( 500a and 500b of Figure 5 ) and the second ethanolamine CRP ( 600 of Figure 6 ), respectively.
  • an anion exchange stationary phase includes a base layer 200 that is reacted with at least about three to about ten reactions cycles of reagents (diepoxide and ethanolamine), and preferably about three to about four reactions cycles of reagents to form a crosslinked ethanolamine polymer layer.
  • the crosslinked ethanolamine condensation polymer layer can be covalently attached to the base condensation polymer.
  • the crosslinked ethanolamine condensation polymer layer includes quaternary ammonium groups, ether groups, and hydroxy groups, as illustrated in Figures 3 to 6 . At least a portion of the ether groups are spaced from the quaternary ammonium groups by a two carbon spacer. Similarly, at least a portion of the hydroxy groups are spaced from the quaternary ammonium groups by the first two carbon spacer.
  • the crosslinked ethanolamine polymer layer can be reacted with a first glycidol and a second glycidol treatment to form the anion exchange stationary phase.
  • the first and second glycidol treatments can each include flowing a solution of the glycidol through the reaction column.
  • a pendant hydroxy group (e.g., 602 ) and/or the secondary amine group (e.g., 604 ) of an ethanolamine CRP (e.g., 600 of Figure 6 ) can be reacted with an epoxide portion of a first glycidol to form a first glycidol CRP ( 700b and 700a ), as illustrated in Figure 7 .
  • the first glycidol CRP ( 700b and 700a ) can be covalently attached to the third ethanolamine condensation product.
  • the first glycidol CRP ( 700b and 700a ) includes a reaction product of i) an amine of the third ethanolamine CRP, and ii) a first glycidol.
  • One pendant dihydroxy group branch 700b can be formed from the pendant hydroxy group (e.g., 602 ) and two pendant dihydroxy group branches 700a can be formed from the secondary amine group (e.g., 604 ).
  • the secondary amine (e.g., 604 ) is converted to a quaternary ammonium group that has a positive charge.
  • hydroxy groups (e.g, 502 ) that are spaced apart from a quaternary ammonium group with a two carbon spacer can be referred to as a beta hydroxy group.
  • beta hydroxy groups e.g., 502
  • beta hydroxy groups can be reactive with epoxy groups of glycidol to form additional dihydroxy group branches.
  • FIG. 8 illustrates beta hydroxy groups 702 being reacted with a second glycidol to form a second glycidol CRP 800 .
  • the second glycidol CRP 800 can be covalently attached to the first glycidol CRP ( 700a and 700b ).
  • the second glycidol CRP 800 includes a reaction product of i) a hydroxy group ( 702 or 704 ) of the first glycidol CRP, in which a portion of the hydroxy groups 702 of the first glycidol CRP is spaced from a quaternary ammonium group of the third ethanolamine condensation reaction product by a two carbon spacer; and ii) a second glycidol.
  • the crosslinked ethanolamine polymer can be treated with a hydroxide solution before each of the first and second glycidol treatments. Such hydroxide solution treatments can deprotonate the beta hydroxy groups to enhance the reactivity with glycidol.
  • the squiggle in Figures 5 to 8 can represent adjacent chemical moieties such as, for example, the base condensation polymer 200 and the first polyepoxide CRP 300 .
  • the crosslinked ethanolamine polymer layer can be reacted with two to ten, and preferably two to four sequential glycidol treatments to form a glycidol condensation layer that is covalently attached to the crosslinked ethanolamine condensation polymer layer.
  • the glycidol condensation layer includes a plurality of dihydroxy groups, in which each dihydroxy group includes a first hydroxy group 702 and a second hydroxy group 704 .
  • the first hydroxy 702 is spaced from the second hydroxy 704 by the first two carbon spacer.
  • At least a portion of the first hydroxy groups 702 is spaced from the quaternary ammonium groups of the crosslinked ethanolamine condensation polymer layer by the first two carbon spacer.
  • the hydroxyalkylamine can be in the form of ethanolamine 106 having a two carbon spacer (e.g., alkyl) with a terminal hydroxy group and terminal amine group.
  • a two carbon spacer e.g., alkyl
  • the hydroxy groups 202 and 302 are both spaced apart from a quaternary ammonium group by a two carbon spacer, which makes the hydroxy groups 202 and 302 more acidic.
  • Hydroxy groups separated from the quaternary ammonium group anion exchange site by a two carbon spacer are more acidic than hydroxy groups spaced apart by a three carbon spacer (gamma position), a four carbon spacer (delta position), or farther relative to the quaternary ammonium group anion exchange site.
  • the pKa of a beta hydroxy group is believed to be about 13.9, which makes it about 100 times more acidic than a hydroxy group not close to a quaternary ammonium group.
  • a model compound choline can be used to illustrate the increased acidity of a beta hydroxy group with respect to a quaternary ammonium group.
  • the hydroxy group of choline has a pKa of 13.9, which is much lower than ethanol, which does not have a proximate quaternary ammonium group.
  • the hydroxy group of ethanol has a pKa of 15.9.
  • the deprotonated and negatively charged beta hydroxy group is stabilized by the proximate positive charge of the quaternary ammonium group, and thus, results in an increased acidity.
  • the deprotonated hydroxy group can act as a stronger reactant for opening the epoxide ring of a glycidol group.
  • the glycidol treatments reduces the population of beta hydroxide groups in the ion exchange resin, and thus, alters the anion binding characteristics of the anion exchange resin.
  • a hydroxide eluent is typically used.
  • the beta hydroxide can be deprotonated causing the ion exchange site to form a zwitterionic ion pair 902 (see e.g., Figure 9 ), which decreases the anion binding of the resin.
  • Zwitterionic ion pair 902 has a positively charged quaternary ammonium group that is stabilized by the negatively charged and deprotonated hydroxy group.
  • anion binding capability of anion exchange resins can be tuned based on the concentration (or pH) of the hydroxide eluent.
  • a 9 ⁇ 250 mm (diameter ⁇ length) reaction column was packed with 6.5 ⁇ m diameter particles with surface sulfonated (one hour at room temperature) 20.8 m 2 /g wide-pore resin (DVB/EVB).
  • the base condensation layer was applied to a packed column by flowing a butanediol diglycidyl ether-methylamine solution mixture (10% (wt/wt%) with respect to butanediol diglycidyl ether: 4% (wt/wt %) with respect to methylamine) at 0.5 mL/minute through the column at 68° C for 60 minutes to form a base condensation polymer 200 (see Figure 2 ).
  • the reagent solutions are prepared in deionized water.
  • 4 cycles of reagent treatment were flowed at 0.5 mL/minute through the column at 68° C.
  • a single cycle of reagent treatment included a first step a) 10% (wt/wt %) butanediol diglycidyl ether solution was flowed through the column for 30 minutes to form a first diepoxide condensation reaction product 300 (see Figure 3 ), a second step b) deionized water was flowed the column for 10 minutes, a third step c) 7.88% (wt/wt %) ethanolamine solution was flowed through column for 30 minutes to form a first ethanolamine condensation reaction product 400 (see Figure 4 ), and a fourth step d) deionized water was flowed the column for 10 minutes.
  • steps a) to d) three additional cycles of reagent treatment were performed.
  • the anion exchange resin with crosslinked ethanolamine was removed from the reaction column into a container. 400 grams of 1 M NaOH was mixed with 20 grams of the anion exchange resin (1:20 ratio of resin to 1M NaOH, wt/wt %) in the container. The mixture was then sonicated to disperse the resin particles at room temperature for 60 minutes and then sieved and filtered. Next, the filter cake was washed with deionized water. The resulting filter cake formed a cleaned-up resin that was packed into 2 ⁇ 250 mm chromatography columns.
  • step 1) deionized water was flowed for 5 minutes at 68° C.
  • step 2) 20% glycidol solution was flowed for 60 minutes at 68° C to form the first glycidol condensation reaction product (e.g., 700a and 700b of Figure 7 ).
  • step 3) deionized water was flowed for 5 minutes at 68° C.
  • step 4) 0.1 M NaOH was flowed at room temperature for 25 minutes.
  • step 5) deionized water was flowed for 5 minutes at 68° C.
  • step 6) 20% glycidol solution was flowed for 60 minutes at 68° C to form the second glycidol condensation reaction product (see 800 of Figure 8 ).
  • step 8) deionized water was flowed for 5 minutes at 68° C.
  • step 1) 0.1 M NaOH was flowed at room temperature for 30 minutes.
  • step 2) deionized water was flowed for 10 minutes at 68° C.
  • step 3) 20% glycidol solution was flowed for 60 minutes at 68° C to form the first glycidol condensation reaction product (e.g., 700a and 700b of Figure 7 ).
  • step 4) deionized water was flowed for 10 minutes at 68° C.
  • step 5) 0.1 M NaOH was flowed at 68° C for 20 minutes.
  • step 6) deionized water was flowed for 10 minutes at 68° C.
  • step 7) 20% glycidol solution was flowed for 60 minutes at 68° C to form the second glycidol condensation reaction product (see 800 of Figure 8 ).
  • step 8) deionized water was flowed for 10 minutes at 68° C.
  • step 9) the anion exchange resin from the reaction column was removed into a container.
  • step 10) 400 grams of 1 M NaOH was mixed with 20 grams of the anion exchange resin (1:20 ratio of resin to 1M NaOH, wt/wt %) in the container, sonicated to disperse the resin particles at room temperature for 60 minutes, and then sieved and filtered.
  • step 11) the filter cake was washed with deionized water. The resulting filter cake formed a cleaned-up resin that was packed into 2 ⁇ 250 mm chromatography columns.
  • IonPac AS24, AS24A, and AS26 are anion exchange stationary phases that each includes a hyperbranched anion-exchange condensation polymer, electrostatically attached to the surface of a sulfonated wide-pore polymeric substrate.
  • IonPac AS26 has alkanol quaternary ammonium functional groups and includes alternating treatments of epoxy monomer and methylamine to produce a coating that grows directly off of the substrate surface.
  • the chromatography column of Examples 3 was also used.
  • a pump was used to pump deionized water into a Thermo Scientific Dionex EGC 500 KOH cartridge (Thermo Fisher Scientific, Sunnyvale, California) for generating a KOH gradient, which was different for each column type.
  • the KOH gradient was optimized for each column to separate sulfate and phosphate from neighboring peaks.
  • a temperature regulator was used to maintain a column temperature of 15 °C.
  • a Dionex AERS 500 suppressor was used along with a Thermo Scientific conductivity detector.
  • Table 1 lists the relevant chromatographic system conditions for each type of chromatography column tested such as flow rate, injection volume, the gradient elution parameters, the suppressor format (for corresponding tubing diameter of the system), and applied current to the suppressor.
  • Table 1 Column Type Flow Rate (mL/min) Injection Volume ( ⁇ L) Time (minutes) KOH Concentration (mM) AERS Format (mm) / Current (mA) IonPac AS24 0.25 2.5 0-7 5 2 / 56 7-16 5-25 16-27 25-90 27-45 90 IonPac AS24A 0.25 2.5 0-7 5 2 / 45 7-15 5-35 15-30 35-45 30-50 45 IonPac AS26 1.0 10 0-7 5 4 / 223 7-16 5-35 16-25 35-90 25-60 90 Example 3 0.25 2.5 0-7 5 2 / 35 7-16 5-25 16-23 25-55 23-40 55
  • Figure 10 illustrates four chromatograms of the standard solution using four different anion exchange resins, which are Thermo Scientific Dionex IonPac chromatography columns AS24, AS24A, AS26, and the column of Example 3 (in order from top to bottom).
  • the chromatogram with the column containing crosslinked ethanolamine with glycidol treatments illustrated a shorter chromatographic run time (under 30 minutes) while partially resolving monochloroacetate and chlorite (peaks 2 and 3), and resolving dibromoacetate and nitrite (peaks 9 and 10).
  • the chromatograms run with IonPac AS24, AS24A, or AS26 required about 10 minutes or more run time to elute tribromoacetate (peak 16), and the three commercial columns failed to provide at least partial resolution for all of the haloacetic acids from important inorganic anions (e.g., nitrite - peak 10).
  • the chromatograms run with IonPac AS24 and AS26 required higher eluent concentration than the column of Example 3.
  • Example 5 Chromatograms of the Standard Solution Containing Various Common Inorganic Anions Comparing Glycidol Treatment In Chromatography Column (Example 2) to Glycidol Treatment In Reaction Column (Example 3)
  • Example 4 An ion chromatography system similar to Example 4 was employed with isocratic elution using a KOH eluent and a standard solution of common inorganic anions.
  • the standard solution contained nine anions, which were fluoride 2.0 mg/L, chlorite 10.0 mg/L, bromate 20.0 mg/L, chloride 5.0 mg/L, sulfate 20.0 mg/L, nitrite 15.0 mg/L, chlorate 20.0 mg/L, bromide 20.0 mg/L, and nitrate 20.0 mg/L.
  • a first chromatogram was performed using the column of Example 2 with 9 mM KOH eluent at 0.25 mL/min.
  • a second chromatogram was performed using the column of Example 3 with 9 mM KOH eluent at 0.25 mL/min. Due to the co-eluting peaks of sulfate and nitrite, a third chromatogram was performed using the column of Example 3 with a higher 12 mM KOH eluent at 0.25 mL/min to separate sulfate and nitrite, so number of plates and asymmetry for sulfate can be measured accurately.
  • the data from the first, second, and third chromatogram were shown in Table 3 below. Table 3.
  • the second chromatogram showed an improvement in the number of plates and asymmetry for bromide compared to the first chromatogram (from 4334 to 6439 plates, and from 1.4 to 1.14).
  • the third chromatogram showed an improvement in the number of plates and asymmetry for sulfate compared to the first chromatogram (from 3259 to 5769 plates, and from 1.27 to 0.99).
  • This chromatography column of Example 3 demonstrates that adding glycidol to the reaction column improves the subsequent packing of the chromatography columns, and results in a higher plate count and lower asymmetry compared to removing the ion exchange resin from the reaction column and then packing the chromatography column that is subsequently reacted with glycidol, as described in Example 2.
  • Example 6 Chromatograms Using Anion Exchange Resins with Smaller Particles.
  • Anion exchange resins were synthesized in manner similar to Example 1 except that three different types of particles were used in the synthesis to create three different resins, which were referred to as A (4.75 micron diameter, 26.3 m 2 /g, 4 hour at 80 °C sulfonation), B (4.55 micron diameter, 27.6 m 2 /g, 4 hour at 80 °C sulfonation), and C (4.6 micron diameter, 17.4 m 2 /g, 1 hour at room temperature sulfonation).
  • the particles used in Example 6 were smaller than Example 1, had different surface areas, and varying levels of sulfonation.
  • Example 6 The anion exchange resins of Example 6 were then treated in a manner similar to Example 3 except that a shorter 2 ⁇ 150 mm chromatography column was used to further accelerate the chromatographic separation.
  • the chromatography columns of Example 6 was tested in an ion chromatography system similar to Example 4.
  • Table 4 lists the relevant chromatographic system conditions for this example such as flow rate, injection volume, the gradient elution parameters, the suppressor format (for corresponding tubing diameter of the system), and applied current to the suppressor. Table 4.
  • Figure 11 illustrates three chromatograms that separated a standard solution listed in Table 5 using three different anion exchange resins, which are represented as A, B, and C of this Example 6.
  • the chromatograms run with anion exchange resins A, B, and C using a smaller particle size had faster run times of about 20 minutes with along with good separation.
  • the chromatographic run times of Example 6 were about 10 minutes faster (50%) compared to the chromatographic run times of Example 4 (see Figure 10 ).
  • Example 6 Anion exchange resins A and C of Example 6 was tested in an ion chromatography system similar to Example 4.
  • Table 6 lists the relevant chromatographic system conditions for this example such as flow rate, injection volume, the gradient elution parameters, the suppressor format (for corresponding tubing diameter of the system), and applied current to the suppressor. Table 6.
  • AERS Format (mm) / Current (mA) A of Example 6 0.25 2.5 0-4 4 2 / 28 4-10 4-15 10-15 15-45 15-25 45
  • C of Example 6 0.25 2.5 0-4 4 2 / 28 4-10 4-18 10-15 18-45 15-25 45
  • Figure 12 illustrates two chromatograms that separated the standard solution listed in Table 7 using anion exchange resins A and C of Example 6.
  • the chromatograms using A and C of Example 6 show the feasibility of resolving all 18 analytes of Table 7. Although a few of the peaks are not completely baseline resolved, Applicant believes that one or more minor adjustments such as adjusting the number of reaction cycles that form the crosslinked ethanolamine polymer layer, the number of glycidol treatments, adjusting the reaction temperature, lengthening the column, adjusting the elution gradient, and chromatographic run temperature will allow all of the peaks to be resolved in a single chromatographic run.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Plural Heterocyclic Compounds (AREA)

Claims (14)

  1. Phase stationnaire d'échange d'anions comprenant :
    a) une particule de substrat chargée négativement ;
    b) une couche de polymère de condensation de base liée à la particule de substrat chargée négativement, la couche de polymère de condensation de base comprenant :
    i) des groupes ammonium quaternaire ;
    ii) des groupes éther ; et
    iii) des groupes hydroxy, dans lesquels au moins une partie des groupes hydroxy sont espacés des groupes ammonium quaternaire par un premier espaceur à deux carbones et la couche de polymère de condensation de base est formée à partir de méthylamine et d'éther diglycidylique de 1 ,4-butanediol ;
    c) une couche de polymère de condensation d'éthanolamine réticulée fixée de manière covalente à la couche de polymère de condensation de base, la couche de polymère de condensation d'éthanolamine réticulée comprend :
    i) des groupes ammonium quaternaire ;
    ii) des groupes éther, dans lesquels au moins une partie des groupes éther sont espacés des groupes ammonium quaternaire par un second espaceur à deux carbones ;
    et
    iii) des groupes hydroxy, dans lesquels au moins une partie des groupes hydroxy sont espacés des groupes ammonium quaternaire par le premier espaceur à deux carbones ;
    et
    d) une couche de condensation de glycidol fixée de manière covalente à la couche de polymère de condensation d'éthanolamine réticulée, la couche de condensation de glycidol comprend : une pluralité de groupes dihydroxy, dans lesquels chaque groupe dihydroxy comporte un premier groupe hydroxy et un second groupe hydroxy, et le premier hydroxy est espacé du second hydroxy par le premier espaceur à deux carbones, dans lequel au moins une partie des premiers groupes hydroxy sont espacées des groupes ammonium quaternaire de la couche polymère de condensation d'éthanolamine réticulée par le premier espaceur à deux carbones.
  2. Phase stationnaire d'échange d'anions selon la revendication 1, dans laquelle la particule de substrat chargée négativement comprend une particule de divinylbenzène et d'éthylvinyl benzène réticulée, dans laquelle au moins une surface de la particule de substrat chargée négativement comporte des groupes sulfonate.
  3. Phase stationnaire d'échange d'anions selon la revendication 1 ou la revendication 2, dans laquelle la couche de polymère de condensation de base est chargée positivement et fixée ioniquement à la particule de substrat chargée négativement.
  4. Phase stationnaire d'échange d'anions selon l'une quelconque des revendications précédentes, dans laquelle le premier espaceur à deux carbones comprend une formule chimique de
    Figure imgb0006
     et le second espaceur à deux carbones comprend une formule chimique de
    Figure imgb0007
  5. Procédé de formation d'une phase stationnaire d'échange d'anions comprenant :
    la réaction d'un éther diglycidylique de 1,4-butanediol avec une méthylamine pour former une couche de polymère de condensation de base sur une particule de substrat chargée négativement ;
    la réaction de la couche de polymère de condensation de base dans un nombre de cycles de réaction pour former une couche de polymère d'éthanolamine réticulée, dans laquelle le nombre de cycles de réaction est compris entre environ trois et environ dix et chaque cycle de réaction comporte un traitement au polyépoxyde suivi d'un traitement à l'éthanolamine ; et
    la réaction de la couche de polymère d'éthanolamine réticulée avec un premier glycidol et ensuite un second glycidol pour former la phase stationnaire d'échange d'anions.
  6. Procédé selon la revendication 5, qui comprend en outre : le traitement de la couche de polymère d'éthanolamine réticulée avec une solution d'hydroxyde avant chacun du premier traitement au glycidol et du second traitement au glycidol.
  7. Procédé selon la revendication 5 ou la revendication 6, dans lequel les particules de substrat chargées négativement sont contenues sous forme de lit tassé dans une première colonne, dans laquelle la réaction de l'éther diglycidylique de 1 ,4-butanediol avec la méthylamine comprend : l'écoulement d'une solution d'éther diglycidylique de 1 ,4-butanediol et de méthylamine à travers la première colonne pour former la couche de polymère de condensation de base sur les particules de substrat chargées négativement.
  8. Procédé selon la revendication 7, dans lequel le traitement au polyépoxyde comprend : l'écoulement d'une solution du polyépoxyde à travers la première colonne ; et le traitement à l'éthanolamine comprend : l'écoulement d'une solution de l'éthanolamine à travers la première colonne.
  9. Procédé selon l'une quelconque parmi les revendications 5 à 8, dans lequel le premier traitement au glycidol et le second traitement au glycidol comprennent chacun : l'écoulement d'une solution du glycidol à travers la première colonne.
  10. Procédé selon l'une quelconque parmi les revendications 5 à 9, dans lequel le nombre de cycles de réaction est compris entre environ 3 et environ 4.
  11. Procédé selon l'une quelconque des revendications 5 à 10, dans lequel la particule de substrat chargée négativement comprend une particule de divinylbenzène et d'éthylvinyl benzène réticulée, dans lequel au moins une surface de la particule de substrat chargée négativement comporte des groupes sulfonates et dans lequel la couche de polymère de condensation de base est chargée positivement et liée ioniquement à la particule de substrat chargée négativement.
  12. Procédé selon l'une quelconque parmi les revendications 5 à 11, dans lequel le polyépoxyde comprend de l'éther diglycidylique de 1,4-butanediol.
  13. Utilisation d'une phase stationnaire d'échange d'anions selon la revendication 1 destinée à séparer des acides halogénoacétiques en présence d'anions inorganiques.
  14. Utilisation selon la revendication 13 d'une phase stationnaire d'échange d'anions, l'utilisation comprenant :
    l'écoulement d'un éluant à travers une colonne de chromatographie, la colonne de chromatographie contenant la phase stationnaire d'échange d'anions, dans laquelle l'éluant comporte un hydroxyde ; et
    de préférence dans laquelle le procédé comprend en outre :
    la séparation d'au moins un analyte d'un échantillon injecté dans la colonne de chromatographie.
EP19164250.3A 2018-03-22 2019-03-21 Phases stationnaires d'échange d'anions à base de couche d'hydroxyalkylamine réticulée et de glycidol Active EP3542902B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US15/928,384 US10773254B2 (en) 2018-03-22 2018-03-22 Anion exchange stationary phases based on crosslinked hydroxyalkylamine layer and glycidol
US16/101,264 US10766026B2 (en) 2018-08-10 2018-08-10 Anion exchange stationary phases based on crosslinked hydroxyalkylamine layer and glycidol

Publications (2)

Publication Number Publication Date
EP3542902A1 EP3542902A1 (fr) 2019-09-25
EP3542902B1 true EP3542902B1 (fr) 2023-05-17

Family

ID=65904154

Family Applications (2)

Application Number Title Priority Date Filing Date
EP19164250.3A Active EP3542902B1 (fr) 2018-03-22 2019-03-21 Phases stationnaires d'échange d'anions à base de couche d'hydroxyalkylamine réticulée et de glycidol
EP19164245.3A Active EP3542901B1 (fr) 2018-03-22 2019-03-21 Phases stationnaires d'échange d'anions basées sur une couche d'hydroxyalkylamine réticulée et de glycidol

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP19164245.3A Active EP3542901B1 (fr) 2018-03-22 2019-03-21 Phases stationnaires d'échange d'anions basées sur une couche d'hydroxyalkylamine réticulée et de glycidol

Country Status (2)

Country Link
EP (2) EP3542902B1 (fr)
CN (2) CN110292957B (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112756016A (zh) * 2020-12-11 2021-05-07 安徽皖仪科技股份有限公司 一种接枝型阴离子交换树脂色谱填料及其制备方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0883574B1 (fr) * 1996-03-01 2004-01-02 Dionex Corporation Resines d'echange d'anions portant au moins deux groupes differents d'echange d'ions contenant de l'azote
US6881761B2 (en) * 2000-05-29 2005-04-19 Showa Denko K.K. Porous polymer particle, anion exchanger, producing method thereof, column for ion chromatography, and method for measuring anions
US7291395B2 (en) * 2004-02-18 2007-11-06 Dionex Corporation Coated ion exchanged substrate and method of forming
US8101422B2 (en) 2005-09-16 2012-01-24 Dionex Corporation Multidimensional chromatography apparatus and method
US7968663B2 (en) * 2007-12-18 2011-06-28 General Electric Company Anion exchange polymers, methods for making and materials prepared therefrom
US9132364B2 (en) * 2010-02-26 2015-09-15 Dionex Corporation High capacity ion chromatography stationary phases and method of forming
JP2013545595A (ja) * 2010-10-15 2013-12-26 シーメンス インダストリー インコーポレイテッド アニオン交換膜及び製造方法
US9034447B2 (en) * 2011-03-11 2015-05-19 Dionex Corporation Electrostatically bound hyperbranched anion exchange surface coating prepared via condensation polymerization using ditertiary amine linkers for improved divalent anion selectivity
US9486799B2 (en) * 2012-09-11 2016-11-08 Dionex Corporation Glycidol functionalized anion exchange stationary phases

Also Published As

Publication number Publication date
EP3542901B1 (fr) 2020-11-25
EP3542902A1 (fr) 2019-09-25
CN110292956A (zh) 2019-10-01
EP3542901A1 (fr) 2019-09-25
CN110292956B (zh) 2022-12-06
CN110292957A (zh) 2019-10-01
CN110292957B (zh) 2022-12-09

Similar Documents

Publication Publication Date Title
US9486799B2 (en) Glycidol functionalized anion exchange stationary phases
US9278297B2 (en) Method for ion-exchange chromatography and media used thereof
EP3542902B1 (fr) Phases stationnaires d'échange d'anions à base de couche d'hydroxyalkylamine réticulée et de glycidol
US10773254B2 (en) Anion exchange stationary phases based on crosslinked hydroxyalkylamine layer and glycidol
Darko et al. Large-scale flow photochemical synthesis of functionalized trans-cyclooctenes using sulfonated silica gel
US10766026B2 (en) Anion exchange stationary phases based on crosslinked hydroxyalkylamine layer and glycidol
EP3714976A1 (fr) Support de chromatographie à échange d'anions hydrophile
EP3479900B1 (fr) Phases stationnaires d'échange d'ions pour analyse d'ions polyvalents
JP2011053174A (ja) 陽イオンの分析法
EP3816623A1 (fr) Colonnes de chromatographie à gradient longitudinal
EP3603808B1 (fr) Phases stationnaires d'échange d'anions basées sur une couche polymère de polyalkylpolyamine
Zatirakha et al. Novel stationary phases for ion chromatography and hydrophilic interaction liquid chromatography
CN106955505A (zh) 交联琼脂糖凝胶分离材料的制备

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN PUBLISHED

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20200324

RBV Designated contracting states (corrected)

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

17Q First examination report despatched

Effective date: 20200518

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTG Intention to grant announced

Effective date: 20221202

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602019028997

Country of ref document: DE

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 1568192

Country of ref document: AT

Kind code of ref document: T

Effective date: 20230615

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG9D

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20230517

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 1568192

Country of ref document: AT

Kind code of ref document: T

Effective date: 20230517

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230918

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230817

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: RS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230917

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230818

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602019028997

Country of ref document: DE

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20240220

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20240315

Year of fee payment: 6

Ref country code: GB

Payment date: 20240314

Year of fee payment: 6

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230517